CN106893093A - The batch production equipment and preparation method of a kind of graphene composite material - Google Patents
The batch production equipment and preparation method of a kind of graphene composite material Download PDFInfo
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- CN106893093A CN106893093A CN201710222714.0A CN201710222714A CN106893093A CN 106893093 A CN106893093 A CN 106893093A CN 201710222714 A CN201710222714 A CN 201710222714A CN 106893093 A CN106893093 A CN 106893093A
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 104
- 229910021389 graphene Inorganic materials 0.000 title claims abstract description 102
- 239000002131 composite material Substances 0.000 title claims abstract description 61
- 238000002360 preparation method Methods 0.000 title claims abstract description 44
- 238000010923 batch production Methods 0.000 title claims abstract description 24
- 239000000463 material Substances 0.000 claims abstract description 117
- 239000002994 raw material Substances 0.000 claims abstract description 67
- 239000004952 Polyamide Substances 0.000 claims abstract description 61
- 229920002647 polyamide Polymers 0.000 claims abstract description 61
- 239000000178 monomer Substances 0.000 claims abstract description 41
- 238000006243 chemical reaction Methods 0.000 claims abstract description 33
- 238000002844 melting Methods 0.000 claims abstract description 26
- 230000008018 melting Effects 0.000 claims abstract description 26
- 239000000839 emulsion Substances 0.000 claims abstract description 20
- 150000001875 compounds Chemical class 0.000 claims abstract description 17
- 238000002156 mixing Methods 0.000 claims abstract description 11
- 239000006185 dispersion Substances 0.000 claims description 20
- 230000000694 effects Effects 0.000 claims description 15
- 238000002604 ultrasonography Methods 0.000 claims description 9
- 150000001412 amines Chemical class 0.000 claims description 5
- 230000001804 emulsifying effect Effects 0.000 claims 1
- 239000002023 wood Substances 0.000 claims 1
- 238000003756 stirring Methods 0.000 abstract description 12
- 230000002349 favourable effect Effects 0.000 abstract description 7
- 238000009776 industrial production Methods 0.000 abstract description 5
- 238000012360 testing method Methods 0.000 description 25
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 14
- 238000000034 method Methods 0.000 description 14
- 238000007142 ring opening reaction Methods 0.000 description 9
- 239000003795 chemical substances by application Substances 0.000 description 7
- 238000006116 polymerization reaction Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000007599 discharging Methods 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- 239000003063 flame retardant Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000004753 textile Substances 0.000 description 3
- 239000012745 toughening agent Substances 0.000 description 3
- 241000222122 Candida albicans Species 0.000 description 2
- 229920002943 EPDM rubber Polymers 0.000 description 2
- 239000004593 Epoxy Substances 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 230000006750 UV protection Effects 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 125000003368 amide group Chemical group 0.000 description 2
- 150000001408 amides Chemical class 0.000 description 2
- 239000003963 antioxidant agent Substances 0.000 description 2
- 230000003078 antioxidant effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229940095731 candida albicans Drugs 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
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- 239000013078 crystal Substances 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
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- 238000011156 evaluation Methods 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 125000000524 functional group Chemical group 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- -1 graphite Alkene Chemical class 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 150000003951 lactams Chemical class 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- 239000004014 plasticizer Substances 0.000 description 2
- 239000012744 reinforcing agent Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 206010054949 Metaplasia Diseases 0.000 description 1
- 229920006152 PA1010 Polymers 0.000 description 1
- 239000004642 Polyimide Substances 0.000 description 1
- 241000295644 Staphylococcaceae Species 0.000 description 1
- 241000191967 Staphylococcus aureus Species 0.000 description 1
- 238000005411 Van der Waals force Methods 0.000 description 1
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- 230000005540 biological transmission Effects 0.000 description 1
- 150000001721 carbon Chemical group 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
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- 238000005119 centrifugation Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
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- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 150000004985 diamines Chemical class 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000007306 functionalization reaction Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 230000015689 metaplastic ossification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002114 nanocomposite Substances 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 150000003014 phosphoric acid esters Chemical class 0.000 description 1
- XNGIFLGASWRNHJ-UHFFFAOYSA-L phthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC=C1C([O-])=O XNGIFLGASWRNHJ-UHFFFAOYSA-L 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 238000006068 polycondensation reaction Methods 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920001721 polyimide Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/04—Carbon
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Polyamides (AREA)
Abstract
A kind of batch production equipment of graphene composite material, it is related to field of compound material, including raw material preparation facilities and reaction unit, the discharge end of raw material preparation facilities is connected to reaction unit, raw material preparation facilities includes the raw materials melt kettle for melting and mixing with Graphene monomer of polyamide, and raw materials melt kettle is provided with high-shear emulsion machine and ultrasonic dispersers.The batch production equipment can be during monomer of polyamide be prepared, by high shear stirring and the synergy of ultrasonic disperse, Graphene is better dispersed in the monomer of polyamide, to obtain the graphene composite material of favorable dispersibility, every excellent.A kind of preparation method of graphene composite material, which solves graphene composite material in large-scale industrial production, the problem of the bad dispersibility for existing.Graphene high-efficiency can be scattered in polyamide, so as to obtain favorable dispersibility, the graphene composite material of every excellent.
Description
Technical field
The present invention relates to field of compound material, set in particular to a kind of batch production of graphene composite material
Standby and preparation method.
Background technology
Graphene is the two-dimentional monoatomic layer carbon material formed by sp2 hydbridized carbon atoms.It has excellent electric property,
Hot property, mechanical performance and biological relevance, have a wide range of applications.Graphene can be as ideal when preparing composite
Nano filling, is combined using the excellent characteristic of Graphene with other materials, can assign material excellent property.Therefore,
Graphene composite material rapidly becomes the focus in nano composite material research field.
Polyamide is commonly called as nylon, and it is the general name of the high polymer containing amide group in macromolecular main chain repeat unit.Its
Itself has good combination property, including mechanical property, heat resistance, wear resistance, chemical proofing and self lubricity etc.,
It is the important macromolecular material of a class.When enhancing phase of the Graphene as polyamide, by between Graphene and polyamide
High-specific surface area and strong adhesive force, the correlated performance of nylon, such as crystal property, heat can be improved using the excellent specific property of Graphene
Stability, conduction, heat conduction and mechanical property etc., to expand the range of application of polyamide material.Thus, Graphene/polyamide is multiple
The research of condensation material is increasingly valued by people.
At present, the method for preparing Graphene/polyamide compoiste material mainly has two kinds：Melt-blending process and in-situ polymerization
Method.Wherein, situ aggregation method is that Graphene is added in reaction vessel together with monomer of polyamide, then by polymerisation come
To required composite.Using the method, dispersion and compatibility of the graphene nanometer sheet in polyimide matrix can be solved
Problem, obtains the composite of favorable dispersibility.
But in the prior art, Graphene and polyamide in-situ polymerization are face realization under lab, can not yet be realized
Industrialization large-scale production.How Graphene to be introduced in the industrialized polymerization process of existing polyamide, and by graphite
Alkene is efficiently scattered in polyamide, is the industrialized production for realizing Graphene polyamide compoiste material, the problem to be solved.
The content of the invention
It is an object of the invention to provide a kind of batch production equipment of graphene composite material, its is rationally distributed, if
Standby succinct, dispersion effect is high, and production efficiency is high.Efficiently grapheme material can be scattered in polyamide, realize Graphene
The large-scale industrial production of composite.
Another object of the present invention is to provide a kind of preparation method of graphene composite material, its method is simple, operation
It is convenient, efficiently grapheme material can be scattered in polyamide, realize the large-scale industry metaplasia of graphene composite material
Produce.
What embodiments of the invention were realized in：
A kind of batch production equipment of graphene composite material, including raw material preparation facilities and reaction unit, raw material system
The discharge end of standby device is connected to reaction unit, and raw material preparation facilities includes being used to melt monomer of polyamide and be mixed with Graphene
The raw materials melt kettle of conjunction, raw materials melt kettle is provided with high-shear emulsion machine and ultrasonic dispersers.
A kind of preparation method of graphene composite material, including：Monomer of polyamide and grapheme material are added to raw material
Melted in molten-bath, and peeled off under the collective effect of high-shear emulsion machine and ultrasonic dispersers and disperseed to mix
Close, obtain compound；Compound is delivered in reaction unit carries out polymerisation, obtains graphene composite material.
The beneficial effect of the embodiment of the present invention is：Set the invention provides a kind of batch production of graphene composite material
It is standby, including raw material preparation facilities and reaction unit.Raw material preparation facilities includes raw materials melt kettle, and raw materials melt kettle is provided with height and cuts
Cut mulser and ultrasonic dispersers.The batch production equipment can be entered during monomer of polyamide is prepared to raw material
While row melting, by high shear stirring and the synergy of ultrasonic disperse, Graphene is better dispersed in polyamide
In monomer, and favorable dispersibility, the graphene composite material of every excellent are further obtained by polymerisation.
The invention provides a kind of preparation method of graphene composite material.Exist present method solves graphene composite material
In large-scale industrial production, the problem of the bad dispersibility for existing.It uses the batch production of above-mentioned graphene composite material
Equipment, in preparation process, by being used in combination for high shear stirring and ultrasonic disperse, polyamides is scattered in by graphene high-efficiency
In amine, so as to obtain favorable dispersibility, the graphene composite material of every excellent.
Brief description of the drawings
Technical scheme in order to illustrate more clearly the embodiments of the present invention, below will be attached to what is used needed for embodiment
Figure is briefly described, it will be appreciated that the following drawings illustrate only certain embodiments of the present invention, thus be not construed as it is right
The restriction of scope, for those of ordinary skill in the art, on the premise of not paying creative work, can also be according to this
A little accompanying drawings obtain other related accompanying drawings.
A kind of flow of the batch production equipment of graphene composite material that Fig. 1 is provided by the embodiment of the present invention 1 is shown
It is intended to.
Icon：100- batch production equipment；110- raw material preparation facilities；111- raw materials melt kettles；112- auxiliary material basins；
113- mixed melting kettles；114- high-shear emulsion machines；115- ultrasonic dispersers；116- by-pass lines；117- feedstock transportation pipelines；
118- auxiliary material conveyance conduits；119- feeding pipes；120- reaction units；121- reactors；130- tanks；140- pelleters.
Specific embodiment
To make the purpose, technical scheme and advantage of the embodiment of the present invention clearer, below will be in the embodiment of the present invention
Technical scheme be clearly and completely described.Unreceipted actual conditions person, builds according to normal condition or manufacturer in embodiment
The condition of view is carried out.Agents useful for same or the unreceipted production firm person of instrument, are the conventional product that can be obtained by commercially available purchase
Product.
The batch production equipment and preparation method to a kind of graphene composite material of the embodiment of the present invention are entered below
Row specific description.
A kind of batch production equipment of graphene composite material, including raw material preparation facilities and reaction unit, raw material system
The discharge end of standby device is connected to reaction unit, and raw material preparation facilities includes being used to melt monomer of polyamide and be mixed with Graphene
The raw materials melt kettle of conjunction, raw materials melt kettle is provided with high-shear emulsion machine and ultrasonic dispersers.
Further, in other preferred embodiments of the invention, raw material preparation facilities is also used to including at least one will be auxiliary
The auxiliary material basin that material, monomer of polyamide mix with Graphene, auxiliary material basin is provided with high-shear emulsion machine and ultrasonic dispersers.
Further, in other preferred embodiments of the invention, raw material preparation facilities also includes mixed melting kettle, and raw material melts
The discharge end for melting kettle is connected by the feed end of feedstock transportation pipeline mixed melting kettle, and the discharge end of auxiliary material basin is defeated by auxiliary material
Pipeline is sent to be connected with the feed end of mixed melting kettle, the discharge end of mixed melting kettle is connected with reaction unit.
Further, in other preferred embodiments of the invention, connected between the discharge end and feed end of raw materials melt kettle
There is by-pass line, by-pass line is provided with for material in pipe to be carried out into ultrasonic stripping and scattered ultrasonic dispersers.
Further, in other preferred embodiments of the invention, raw material preparation facilities passes through feeding pipe and reaction unit
Feed end connection, feeding pipe be provided with for will pipe in material carry out ultrasonic stripping and scattered ultrasonic dispersers.
A kind of preparation method of graphene composite material, including：Monomer of polyamide and grapheme material are added to raw material
Melted in molten-bath, and peeled off under the collective effect of high-shear emulsion machine and ultrasonic dispersers and disperseed to mix
Close, obtain compound.
Wherein, the quality of grapheme material accounts for the 0.05~1% of the monomer of polyamide.By the creative work of inventor
And the experience invented is combined, and drawing in the proportion, the dispersion effect of grapheme material is preferable, the Graphene for obtaining
The performance of composite is more preferably.
Graphene is a kind of cellular flat film formed with sp2 hybrid forms by carbon atom, is a kind of only one of which
The quasi- two-dimensional material of atomic layer level thickness, so be called doing monoatomic layer graphite.Its thickness is about 0.335nm, according to preparation
Mode difference and there are different fluctuatings, generally in height about 1nm or so of vertical direction, horizontal direction width is about
10nm to 25nm, is the basic structural unit of all carbon crystals in addition to diamond.
In present pre-ferred embodiments, grapheme material includes functionalization graphene, graphene oxide and pure Graphene
In one or more.The chemical stability of the pure Graphene of structural integrity is high, the inert state in its surface, with other media
The interaction of (such as solvent) is weaker, and has stronger Van der Waals force between graphene film and piece, easily produces aggregation.And
By introducing specific functional group, can not only strengthen the dispersiveness of Graphene, can also impart to the new property of Graphene, enter one
Step expands its application field.In the present invention, these specific functional groups include but is not limited to acid amides, amino, carboxyl, sulfonic acid
Base, epoxy radicals, hydroxyl etc..
Meanwhile, polyamide is the general name of the high polymer containing amide group in macromolecular main chain repeat unit.It has good
Good combination property, including mechanical property, heat resistance, wear resistance, chemical proofing and self lubricity, and coefficient of friction
It is low, there is certain anti-flammability, it is easy to process, it is suitable to, with other filler filling enhancing modifieds, improve performance and expand range of application.
In an embodiment of the present invention, during polyamide includes but is not limited to PA6, PA66, PA11, PA12, PA610, PA1010 and PA46
Any one.
In embodiments of the present invention, raw materials melt kettle is provided with high-shear emulsion machine and ultrasonic dispersers, when completion polyamides
After the melting of amine monomers, raw material can sufficiently be mixed and is surpassed under the collective effect of high shear stirring and ultrasound
Sound is peeled off and disperseed.
Preferably, between the discharge end and feed end of raw materials melt kettle, it is additionally provided with by-pass line.Polyamides after melting
Amine monomers and grapheme material enter by-pass line by the discharge end of molten-bath, and return to molten-bath reality by the feed end of molten-bath
Now circulate.Meanwhile, in cyclic process, ultrasonic stripping is carried out to the compound in by-pass line by ultrasonic dispersers and is divided
Dissipate.Allow grapheme material further to peel off and disperse, and sufficiently mixed with monomer of polyamide with nanomorphic.
Further, in other preferred embodiments of the invention, in the preparation process of graphene composite material, also wrap
Include the conventional auxiliary material in addition polyamide synthesis.Auxiliary material include plasticizer, toughener, fire retardant, antioxidant, reinforcing agent and
At least one in toner.Preferably, the quality of auxiliary material accounts for the 1~8% of monomer of polyamide and grapheme material summation.
Plasticizer can increase the plasticity of polyamide, so as to be allowed to easy to process and make product that there is flexibility, including
Phthalate, binary acid esters, epoxy ester series, phosphoric acid ester, polyesters, phenyl alkylsulf class and chlorinated paraffin class
Deng.Toughener can improve the impact strength of material, allow material more toughness.In the present invention, toughener is including PP, PE etc.
The elastomer such as nonpolar polyolefin hydrocarbon materials and ethylene propylene diene rubber (EPDM), ethylene-octene copolymer (POE).Fire retardant can be with
Increase the fire resistance of material, and antioxidant can then increase the ageing resistace of material.Reinforcing agent then can be from antistatic
The many aspects such as property, antibiotic property, wearability are further improved the property of material.
In embodiments of the present invention, in order to more uniformly add auxiliary material, can be by auxiliary material, monomer of polyamide and Graphene
Material is melted and is pre-mixed in auxiliary material basin, wherein, the quality of grapheme material is the auxiliary material in auxiliary material basin and poly-
The 0.1~1% of amide monomer gross mass.Auxiliary material basin is again provided with high-shear emulsion machine and ultrasonic dispersers, can be to auxiliary
Grapheme material and auxiliary material in material basin carry out sufficiently ultrasound and peel off dispersion and mix.Preferably, auxiliary material basin can join
The mode for examining raw materials melt kettle sets by-pass line auxiliary material and grapheme material can more uniformly be mixed.Further
Ground, auxiliary material basin can set multiple.In actual production, the bulky of raw materials melt kettle, stirring difficulty is larger, and auxiliary material
The small volume of basin, being capable of more high-effect high-quality ground stirring.By setting multiple auxiliary material basins, dispersion is can be very good former
Expect the stirring pressure of molten-bath, allowing between monomer of polyamide and grapheme material more fully to mix.Meanwhile, multiple auxiliary materials
Basin may be respectively used for introducing multiple auxiliary materials, allow various auxiliary materials to be well dissolved into system.
After monomer of polyamide and auxiliary material are sufficiently mixed with grapheme material respectively, it is delivered in mixed melting kettle, and
Most monomer of polyamide, grapheme material and the abundant melting mixing of auxiliary material three and there is preliminary ring-opening reaction at last, then convey
Polymerisation is carried out into reaction unit.
A kind of preparation method of graphene composite material provided by the present invention also includes：Compound is delivered to reaction dress
Polymerisation is carried out in putting, graphene composite material is obtained.
Compound is delivered to reaction unit by feeding pipe, meanwhile, feeding pipe is provided with ultrasonic dispersers, Ke Yi
During conveying, the dispersiveness of grapheme material is kept, and grapheme material is further peeled off and disperseed, make completion
The graphene composite material obtained after polymerisation evenly, performance more preferably.In course of conveying dispersion is kept using ultrasound
The technology of property, be inventor in order to adapt to large-scale industrial production, createed with reference to experience and creative work
Technical scheme, be inventor itself crystallization of wisdom.
Different according to polyamide types, the synthesis of polyamide can be obtained by polymerization after lactams open loop, may also be by
It is polymerized between diamine and binary acid and obtains.By taking PA6 as an example, caprolactam is mixed with ring opening agent, be heated to all fusings and throw
Enter in polymerisation, when polymerisation starts, caprolactam reacts open loop with ring opening agent, and the caprolactam after open loop gathers again
Conjunction obtains PA6.Preferably, the quality of ring opening agent is the 0.1~1% of the quality of caprolactam, heat the temperature of melting for 120~
200℃。
Further, the condition of polymerisation is：4~6h is reacted at 240~300 DEG C.When the reaction is finished, tune is vacuumized
After whole viscosity and molecular weight balanced reaction, 200~230 DEG C of dischargings are cooled to.Preferably, the relative viscosity of adjustment system is to 2.2
In the range of~3.4, discharging can be easy to working process with the mobility of guarantee system in the range of viscosities, meanwhile, obtain
The dispersion effect of product is more preferably.0~45 DEG C is cooled to by tank after discharging, and it is stand-by to cut into slices.
It is worth noting that, in embodiments of the present invention, the speed of agitator of the high-shear emulsion machine for being used >=500r/
min.In the range of speeds, ensure that Graphene and monomer of polyamide have more preferable dispersion effect.Revolved at a high speed by rotor
Turn the powerful kinetic energy that produced high tangential velocity and high frequency mechanical effect are brought, make material in the narrow gap of stator and rotor
By the comprehensive function such as strong machinery and aquashear, centrifugation extruding, liquid layer friction, shock tear and turbulent flow, so that stone
Black alkene and monomer of polyamide moment uniform, fine ground dispersion and emulsion, and moving in circles by high frequency, finally give the mixed of stabilization
Compound.It is worth noting that, in other preferred embodiments of the invention, emulsification cutter can with skin grinder or other can
Reach the equipment replacement of same stirring and dispersion effect.
Meanwhile, in the present invention, the ultrasonic power of the ultrasonic dispersers for being used is 1~20kW.The power bracket is hair
A person of good sense combines experience and creative work, the preferable stripping for obtaining and dispersion condition.Under the power bracket, cut by height
Cut stirring and ultrasound peel off scattered synergy, it is ensured that Graphene in the course of the polymerization process, with the dispersion of suitable nanomorphic,
It is bound on polyamide molecule chain.Preferably, a length of 30~120min when ultrasound peels off scattered.In the time range,
It is obtained in that and preferably peel off and dispersion effect.
Feature of the invention and performance are described in further detail with reference to embodiments.
Embodiment 1
The present embodiment provides a kind of batch production equipment 100 for preparing graphene composite material, as shown in figure 1,
Including raw material preparation facilities 110 and reaction unit 120, the discharge end of raw material preparation facilities 110 is connected to reaction unit 120.
Shown in reference picture 1, raw material preparation facilities 110 includes raw materials melt kettle 111, auxiliary material basin 112 and mixed melting kettle
113.Raw materials melt kettle 111 is that monomer of polyamide is melted and carries out the preliminary place for mixing with grapheme material.Itself
Possess heating function, the monomer of polyamide and Graphene can be allow preferably to mix the molten monomer of polyamide.Raw material
Molten-bath 111 is provided with high-shear emulsion machine 114, can be in directly the polymer of molten condition to the inside of raw materials melt kettle 111
Monomer and grapheme material carry out high shear stirring, the two is sufficiently mixed.Meanwhile, raw materials melt kettle 111 also sets up
There are ultrasonic dispersers 115, ultrasonic stripping and dispersion can be carried out to the grapheme material in raw materials melt kettle 111, make Graphene
Material can be sufficiently mixed with nm regime with the monomer of polyamide.
In the present embodiment, the discharge end of raw materials melt kettle 111 is connected to raw materials melt kettle 111 by by-pass line 116
Feed end.Preferably peel off and dispersion effect to be pursued, by-pass line 116 is provided with for material in pipe to be carried out into ultrasound
Peel off and scattered ultrasonic dispersers 115.Polymer monomer and grapheme material are in by-pass line 116 and raw materials melt kettle 111
Between circulate, and realize that synchronizing ultrasound is peeled off and disperseed in raw materials melt kettle 111 and by-pass line 116, can more preferable shape
Into the grapheme material of nanomorphic, and it is well dispersed in the monomer of polyamide.
Further, auxiliary material basin 112 is to carry out various auxiliary materials and monomer of polyamide and grapheme material to melt and first
Walk the place of mixing.Auxiliary material basin 112 is again provided with high-shear emulsion machine 114, can directly to auxiliary material basin 112 inside
Auxiliary material, monomer of polyamide and grapheme material carry out high shear stirring, the two is sufficiently mixed.Meanwhile, auxiliary material basin
112 are additionally provided with ultrasonic dispersers 115, it is also possible to carry out ultrasonic stripping and dispersion to the grapheme material in auxiliary material basin 112,
Grapheme material is set to be sufficiently mixed between nm regime and auxiliary material and monomer of polyamide.In the present embodiment, exist
It is same between the discharge end and feed end of auxiliary material basin 112 to set by-pass line 116 to strengthen between grapheme material and auxiliary material
Mixing, obtain more preferably dispersion effect.
Raw materials melt kettle 111 and auxiliary material basin 112 are connected by feedstock transportation pipeline 117 and auxiliary material conveyance conduit 118 respectively
It is connected to mixed melting kettle 113.Mixed melting kettle 113 is likewise supplied with heating function, auxiliary after being pre-mixed with grapheme material respectively
Material and monomer of polyamide, come together in and make in mixed melting kettle 113 further melting mixing mixing, and in mixed melting kettle 113
It is middle to complete preliminary ring-opening reaction.In other preferred embodiments of the invention, mixed melting kettle 113 can also be stirred using high shear
The mode mixed, while ultrasonic dispersers 115 can be set in mixed melting kettle 113, is further carried out to grapheme material
Peel off and disperse.
The discharge end of mixed melting kettle 113 is connected by feeding pipe 119 with the feed end of reaction unit 120.Conveying pipeline
Road 119 is provided with for material in pipe to be carried out into ultrasonic stripping and scattered ultrasonic dispersers 115, can be entered in material and be reacted
Before device 120, the Graphene in it is made further to peel off and is disperseed, and material is further mixed.It is preferred that
Ground, can set measuring pump (not shown) on feeding pipe 119, so as to realize the precise control of inventory, allow into reaction
The material of device 120 can have more preferably reaction effect, make the graphene composite material for finally giving more uniform, and dispersiveness is more
It is good.
Reaction unit 120 can include single or multiple reactors 121.Preferably, reaction unit 120 is connected using multiple
Reactor 121.By the way of series connection, according to the difference of reaction process, and different pressure and temperatures can be used, allow anti-
Should more efficiently carry out.Meanwhile, multiple reactors 121 can also be by the way of parallel connection, and multiple reactors 121 in parallel can
Increase the efficiency of operation to work simultaneously, it would however also be possible to employ alternation maintains the continuity of operation.Specific to the present embodiment
In, the set-up mode of single reactor 121 is only listed, other set-up modes refer to set.
The discharge end of reactor 121 is provided with spinneret (not shown).Graphene composite material after the completion of polymerization passes through
The strip with given shape is formed after spinneret, and is delivered in cold rinse bank 130 and is cooled down.Between the present embodiment is provided
The formula production equipment of having a rest also includes pelleter 140, can carry out pelletizing to the graphene composite material after cooling.
Embodiment 2
The present embodiment provides a kind of graphene composite material, and it uses a kind of Graphene provided in first embodiment to answer
The batch production equipment 100 of condensation material, is obtained by graphene dispersion in polyamide PA6, and its preparation method is as follows：
S1. caprolactam, ring opening agent and Graphene are added in raw materials melt kettle 111,150 DEG C are heated to, until oneself
Lactams all melts.By high-shear emulsion machine 114 and ultrasonic dispersers 115, three is sufficiently mixed.Wherein,
The quality of ring opening agent is the 0.5% of caprolactam, and the quality of Graphene is the 0.5% of caprolactam, high-shear emulsion machine 114
Rotating speed is 600r/min, and ultrasonic power is 10kW, and ultrasonic time is 60min.
S2. auxiliary material (titanium dioxide and water), monomer of polyamide and Graphene are added in auxiliary material basin 112, by height
Emulsification pretreatment machine 114 and ultrasonic dispersers 115, are sufficiently mixed to it.Wherein, the quality of Graphene is auxiliary material and polyamides
The 0.1~1% of amine monomers gross mass, the rotating speed of high-shear emulsion machine 114 is 500r/min, and ultrasonic power is 15kW, when ultrasonic
Between be 30min.
S3. the auxiliary material after being sufficiently mixed in the raw material and S2 after being sufficiently mixed in S1 is passed into mixed melting kettle 113
Being mixed and acted on ring opening agent, in there is preliminary ring-opening reaction at 260 DEG C, being obtained compound.Wherein, the quality of auxiliary material
It is the 1~8% of raw material.
S4. compound is delivered to reactor 121 by feeding pipe 119.During conveying, by ultrasonic dispersers
Material in 115 pairs of feeding pipes 119 is peeled off and disperseed, wherein, ultrasonic power is 20kW.
S5. in reactor 121, in polycondensation reaction is completed at 280 DEG C, viscosity and molecular weight balanced reaction, cooling are adjusted
To 200 DEG C of dischargings, graphene composite material is obtained.
S6. graphene composite material and is delivered to pelleter through spinneret into being cooled to silk in 20 DEG C of cold rinse bank 130
140 are cut into section.
Test example
A kind of graphene composite material provided using embodiment 2 as test sample, to its resistance, bacteriostasis rate, remote
Infrared property, ultraviolet resistance and combustibility are tested, and its specific method of testing is as follows：
1. the test of test sample resistance, using standard GB/T 12014-2009 " antistatic clothing ", to test sample
Tested after carrying out 100 washings, test result is as shown in table 1；
2. the test of test sample bacteriostasis rate, using standard GB/T 20944.3-2008, " antibacterial textile performance is commented
Valency ", after 5 washings are carried out to test sample, is respectively adopted staphylococcus aureus and Candida albicans is tested, and tests
Result is as shown in table 1；
3. the test of test sample far infrared performance, using standard GB/T 30127-2013 " textile far infrared performances
Detection and evaluation ", test sample is carried out 5 times washing after test, test result is as shown in table 1；
4. the test of test sample ultraviolet resistance, using standard GB/T 18830-2009 " textile antiultraviolets
The evaluation of performance ", tests after 5 washings are carried out to test sample, and test result is as shown in table 1；
5. the test of test sample combustibility, using standard GB/T 2408-2008 " the measure water of Plastics Combustion performance
Flat method and normal beam technique ", makes 5 parts of sizes for the bulk sample of 8cm × 1cm × 0.4cm is tested from test sample, tests
Result is as shown in table 2, wherein, t1Represent residual flame time first time, t2Represent second residual flame time, t3Represent third time residual flame
Time.
The graphene composite material the performance test results of table 1.
The graphene composite material combustibility test result of table 2.
As can be seen from Table 1, a kind of resistance of graphene composite material that the embodiment of the present invention 2 is provided reach 1.7 ×
1012Ω, is a kind of good anti-static material.Meanwhile, it has good bacteriostasis, to gold-coloured staphylococci and white
The inhibiting rate of candida albicans is respectively reached>99% and 81%.The graphene composite material is also a kind of good far infrared weaving
Product, its far infrared transmissivity is up to 0.89, and it is 1.4 DEG C that far infrared transmission rises temperature value.Additionally, the graphene composite material also has
Excellent uvioresistant effect, its UPF UPF is more than 50%.As can be seen from Table 2, the institute of the embodiment of the present invention 2
A kind of graphene composite material for providing can reach intrinsic V0 grade fire-retardant rank, while nothing spreads, without dripping off, it has excellent
Different fire resistance.
In sum, the invention provides a kind of batch production equipment of graphene composite material, including prepared by raw material
Device and reaction unit.Raw material preparation facilities includes raw materials melt kettle, and raw materials melt kettle is provided with high-shear emulsion machine and ultrasound
Disperser.The batch production equipment can be led to during monomer of polyamide is prepared, while being melted to raw material
The synergy of too high shear agitation and ultrasonic disperse, Graphene is better dispersed in the monomer of polyamide, and further
By polymerisation, favorable dispersibility, the graphene composite material of every excellent are obtained.Present invention also offers a kind of stone
The preparation method of black alkene composite.Present method solves graphene composite material in large-scale industrial production, exist
The problem of bad dispersibility.It uses the batch production equipment of above-mentioned graphene composite material, in preparation process, is cut by height
Cut stirring and ultrasonic disperse is used in combination, graphene high-efficiency is scattered in polyamide, so as to obtain favorable dispersibility, respectively
The graphene composite material of item excellent.
The preferred embodiments of the present invention are the foregoing is only, is not intended to limit the invention, for the skill of this area
For art personnel, the present invention can have various modifications and variations.It is all within the spirit and principles in the present invention, made any repair
Change, equivalent, improvement etc., should be included within the scope of the present invention.
Claims (10)
1. the batch production equipment of a kind of graphene composite material, including raw material preparation facilities and reaction unit, the raw material
The discharge end of preparation facilities is connected to the reaction unit, it is characterised in that the raw material preparation facilities includes being used for polyamides
The raw materials melt kettle that amine monomers are melted and mixed with Graphene, the raw materials melt kettle is provided with high-shear emulsion machine and ultrasound point
Dissipate device.
2. batch production equipment according to claim 1, it is characterised in that the raw material preparation facilities is also included at least
One is used to the auxiliary material basin for mixing auxiliary material, monomer of polyamide with Graphene, and the auxiliary material basin is provided with high-shear emulsifying
Machine and ultrasonic dispersers.
3. batch production equipment according to claim 2, it is characterised in that the raw material preparation facilities also includes mixing
Molten-bath, the discharge end of the raw materials melt kettle is connected by feedstock transportation pipeline with the feed end of the mixed melting kettle, institute
The discharge end for stating auxiliary material basin is connected by auxiliary material conveyance conduit with the feed end of the mixed melting kettle, the mixed melting kettle
Discharge end be connected with the reaction unit.
4. batch production equipment according to claim 1, it is characterised in that the discharge end of the raw materials melt kettle and enter
Material is connected with by-pass line between end, and the by-pass line is provided with for that will carry out ultrasonic stripping and scattered super by material in pipe
Sound disperser.
5. batch production equipment according to claim 1, it is characterised in that the raw material preparation facilities passes through conveying pipeline
Road is connected with the feed end of the reaction unit, and the feeding pipe is provided with for material in pipe being carried out into ultrasonic stripping and being divided
Scattered ultrasonic dispersers.
6. a kind of preparation method of graphene composite material, it is characterised in that including：Monomer of polyamide is added with grapheme material
Enter in raw materials melt kettle and melted, and peeled off under the collective effect of high-shear emulsion machine and ultrasonic dispersers and
Dispersion mixing, obtains compound；The compound is delivered in reaction unit carries out polymerisation, obtains Graphene composite wood
Material.
7. the preparation method of graphene composite material according to claim 6, it is characterised in that the compound is by described
The discharge end of molten-bath enters by-pass line, and returning to the molten-bath by the feed end of the molten-bath realizes circulation；In circulation
During, ultrasonic stripping and dispersion are carried out to the compound in the by-pass line by ultrasonic dispersers.
8. the preparation method of graphene composite material according to claim 7, it is characterised in that the compound is by defeated
Pipe material is delivered to reaction unit, during conveying, the compound in feeding pipe is surpassed using ultrasonic dispersers
Sound is peeled off and disperseed.
9. the preparation method of graphene composite material according to claim 6, it is characterised in that the high-shear emulsion machine
Speed of agitator >=500r/min.
10. the preparation method of graphene composite material according to claim 8, it is characterised in that ultrasonic dispersers it is super
Acoustical power is 1~20kW.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108323869A (en) * | 2018-02-05 | 2018-07-27 | 北京服装学院 | A kind of graphene far infrared intelligent temperature control sole and shoes |
| CN109513926A (en) * | 2018-12-20 | 2019-03-26 | 昆明理工大学 | A kind of preparation method of the CNT-GO/Cu composite material with hierarchical structure |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101050279A (en) * | 2007-05-09 | 2007-10-10 | 武汉森大科技研究发展中心 | Production technique and equipment for polymerizing polyamide |
| CN101885842A (en) * | 2010-07-09 | 2010-11-17 | 北京三联虹普纺织化工技术有限公司 | Continuous polymerization production technology for polyamide fibre 6 |
| CN104562276A (en) * | 2014-12-05 | 2015-04-29 | 淮安锦纶化纤有限公司 | Method for modifying chinlon 6 fibers and modified product |
| CN105254870A (en) * | 2015-11-04 | 2016-01-20 | 四川大学 | High-performance monomer casting nylon/graphene nanometer composite material and in-situ polymerization preparation method of high-performance monomer casting nylon/graphene nanometer composite material |
| CN105384962A (en) * | 2015-12-21 | 2016-03-09 | 赵社涛 | Carbon black composite material |
| CN105622929A (en) * | 2014-11-06 | 2016-06-01 | 合肥杰事杰新材料股份有限公司 | Casting nylon/graphene nanocomposite material and preparation method thereof |
-
2017
- 2017-04-06 CN CN201710222714.0A patent/CN106893093B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101050279A (en) * | 2007-05-09 | 2007-10-10 | 武汉森大科技研究发展中心 | Production technique and equipment for polymerizing polyamide |
| CN101885842A (en) * | 2010-07-09 | 2010-11-17 | 北京三联虹普纺织化工技术有限公司 | Continuous polymerization production technology for polyamide fibre 6 |
| CN105622929A (en) * | 2014-11-06 | 2016-06-01 | 合肥杰事杰新材料股份有限公司 | Casting nylon/graphene nanocomposite material and preparation method thereof |
| CN104562276A (en) * | 2014-12-05 | 2015-04-29 | 淮安锦纶化纤有限公司 | Method for modifying chinlon 6 fibers and modified product |
| CN105254870A (en) * | 2015-11-04 | 2016-01-20 | 四川大学 | High-performance monomer casting nylon/graphene nanometer composite material and in-situ polymerization preparation method of high-performance monomer casting nylon/graphene nanometer composite material |
| CN105384962A (en) * | 2015-12-21 | 2016-03-09 | 赵社涛 | Carbon black composite material |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108323869A (en) * | 2018-02-05 | 2018-07-27 | 北京服装学院 | A kind of graphene far infrared intelligent temperature control sole and shoes |
| CN109513926A (en) * | 2018-12-20 | 2019-03-26 | 昆明理工大学 | A kind of preparation method of the CNT-GO/Cu composite material with hierarchical structure |
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Denomination of invention: Intermittent production equipment and preparation method for graphene composite materials Effective date of registration: 20231009 Granted publication date: 20171205 Pledgee: Bank of China Limited Changzhou Zhonglou Branch Pledgor: CHANGZHOU HIGHBERY NEW NANO MATERIALS TECHNOLOGY Co.,Ltd. Registration number: Y2023980060255 |